CN203976655U - Full-automatic domestic refuse production organic fertilizer production line - Google Patents
Full-automatic domestic refuse production organic fertilizer production line Download PDFInfo
- Publication number
- CN203976655U CN203976655U CN201420440925.3U CN201420440925U CN203976655U CN 203976655 U CN203976655 U CN 203976655U CN 201420440925 U CN201420440925 U CN 201420440925U CN 203976655 U CN203976655 U CN 203976655U
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- Prior art keywords
- feed
- opening
- discharge port
- communicated
- organic fertilizer
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
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- Processing Of Solid Wastes (AREA)
- Fertilizers (AREA)
Abstract
The utility model discloses a kind of full-automatic domestic refuse production organic fertilizer production line, comprise fermentation system, premixing system, granule system, screening system, drying system, cooling system and title assembling system, the discharge port of fermentation system is communicated with the opening for feed of premixing system, the discharge port of premixing system is communicated with the opening for feed of a system, the granule discharge port of system and the opening for feed of screening system are communicated with, the first discharge port of screening system is communicated with the opening for feed of drying system, the second discharge port of screening system is communicated with the opening for feed of premixing system, the discharge port of drying system is communicated with the opening for feed of cooling system, the discharge port of cooling system is communicated with claiming the opening for feed of assembling system, claim assembling system organic fertilizer particles is weighed and pack sealing.Production efficiency of the present utility model is high, without a dead lift, cost-saving.
Description
Technical field
The utility model relates to fertilizer production field, relates in particular to a kind of automatic production line that adopts domestic refuse to produce fertilizer.
Background technology
Compostable belongs to a kind of of domestic refuse, and Compostable is transported to composting plant after collecting, and becomes thoroughly decomposed by fermentation, the composting process such as microorganism decompositions processes, and becomes organic fertilizer health, tasteless, as the fertilizer of plant with improve soil.
At present, utilizing domestic refuse to produce the modal form of fertilizer is still that manual operation and simple machinery use, manpower turning, a dead lift, labour intensity is large, and labor safety is compared with Customers ' Legal Right, is unfavorable for that heavy industrialization produces automatically, the performance of enterprises is not outstanding, all in little, loose, weak state.This is also a technical bottleneck of restriction household garbage organic fertilizer development, is badly in need of being resolved.
Utility model content
The utility model object is to provide a kind of full-automatic domestic refuse production organic fertilizer production line, and production efficiency is high, without a dead lift, cost-saving.
The utility model technical solution problem adopts following technical scheme: a kind of full-automatic domestic refuse production organic fertilizer production line, comprise fermentation system, premixing system, granule system, screening system, drying system, cooling system and title assembling system, the discharge port of described fermentation system is communicated with the opening for feed of premixing system, by fermentation after mass transport to premixing system, the discharge port of described premixing system is communicated with the opening for feed of a system, mixed pulverulent material is delivered to a system, the described granule discharge port of system and the opening for feed of screening system are communicated with, the organic fertilizer particles of having rolled into a ball is delivered to screening system, the first discharge port of described screening system is communicated with the opening for feed of drying system, qualified organic fertilizer particles is delivered to drying system, the second discharge port of described screening system is communicated with the opening for feed of premixing system, underproof organic fertilizer particles is delivered to premixing system, the discharge port of described drying system is communicated with the opening for feed of cooling system, organic fertilizer particles after drying is delivered to cooling system, the discharge port of described cooling system is communicated with claiming the opening for feed of assembling system, described title assembling system is weighed organic fertilizer particles and is packed sealing.
Optionally, described system comprises a machine and fly-ash separator, described machine comprises housing, tripper, ball nozzle, loading head and hot-air drier, described tripper, ball nozzle, loading head and hot-air drier are all fixedly mounted in housing, at the top of described housing, offer an opening for feed, under described opening for feed, tripper is set, it is conical that described tripper is, the tip of tripper is over against opening for feed, described ball nozzle be positioned at tripper under, described loading head be positioned at ball nozzle under, described loading head is funnel-form, the diameter of the opening for feed of described loading head upper end is greater than the diameter of the lower surface of tripper, described hot-air drier is positioned at the below of loading head, the air outlet of hot-air drier is horizontally disposed with, the air outlet of hot-air drier is over against the discharge port of loading head below, bottom at described housing is installed with baffle plate, described baffle plate is divided into particle chamber and powder chamber by the bottom of housing inner chamber, described baffle plate is positioned at the below of hot-air drier, described particle chamber be positioned at loading head discharge port under, described powder chamber is positioned at the side-lower of the discharge port of loading head, the air outlet of described hot-air drier be positioned at particle chamber directly over, and the air outlet of hot-air drier is one side setting towards powder chamber, discharge of fine material mouth is offered in the below in described powder chamber, described discharge of fine material mouth is connected with fly-ash separator by induced draft fan, the below in described particle chamber is provided with particulate matter discharge port, described particulate matter discharge port is communicated with the opening for feed of screening system.
Optionally, the discharge port of described fermentation system is communicated with the opening for feed of premixing system by the first conveyor, the discharge port of described premixing system is communicated with the opening for feed of a system by the second conveyor, the discharge port of described system is communicated with the opening for feed of screening system by the 3rd conveyor, the second discharge port of described screening system is communicated with the opening for feed of premixing system by the 4th conveyor, and the discharge port of described cooling system is communicated with claiming the opening for feed of assembling system by the 5th conveyor.
Optionally, also comprise burner, the air outlet of described fermentation system is communicated with the fuel inlet of burner, and the biogas that fermentation system is produced is delivered to burner, and the hot-blast outlet of described burner is communicated with the inlet mouth of hot-air drier and the hot air intake of drying system of granule system respectively.
Optionally, described cooling system comprises feed screw and blower fan, on the air outlet of described blower fan, is fixedly connected with blowpipe, and the other end of described air outlet tube gos deep in the opening for feed of feed screw.
Optionally, described blower fan is cold blast engine.
Optionally, also comprise Controlling System, described Controlling System and first, second, third, fourth, the 5th conveyor are connected.
The utlity model has following beneficial effect: the utility model is connected to a production line by fermentation system, premixing system, a system, screening system, drying system, cooling system and title assembling system, not needing manpower to turn over pushes away and a dead lift, only need the operation of a small amount of workman's production control line, improve production efficiency, saved production cost.
Accompanying drawing explanation
Fig. 1 is the structural representation of the full-automatic domestic refuse production of the utility model organic fertilizer production line;
Fig. 2 is the structural representation of the granule system of the full-automatic domestic refuse production of the utility model organic fertilizer production line;
In figure, mark is illustrated as: 10-fermentation system; 20-premixing system; 30-granule system; 31-granule machine; 32-housing; 33-tripper; 34-ball nozzle; 35-loading head; 36-hot-air drier; 37-granule opening for feed; 38-baffle plate; 39-powder chamber; 40-particle chamber; 41-discharge of fine material mouth; 42-particulate matter discharge port; 50-screening system; 60-drying system; 70-cooling system; 80-claims assembling system; 90-burner.
Embodiment
Below in conjunction with embodiment and accompanying drawing, the technical solution of the utility model is further elaborated.
Embodiment 1
As shown in Figure 1, the present embodiment provides a kind of full-automatic domestic refuse production organic fertilizer production line, comprises fermentation system 10, premixing system 20, a system 30, screening system 50, drying system 60, cooling system 70 and claims assembling system 80.The discharge port of fermentation system 10 is communicated with the opening for feed of premixing system 20, by fermentation after mass transport to premixing system 20, the discharge port of premixing system 20 is communicated with the opening for feed of a system 30, mixed pulverulent material is delivered to a system, the discharge port of granule system 30 is communicated with the opening for feed of screening system 50, the organic fertilizer particles of having rolled into a ball is delivered to screening system 50, the first discharge port of screening system 50 is communicated with the opening for feed of drying system 60, qualified organic fertilizer particles is delivered to drying system 60, the second discharge port of screening system 50 is communicated with the opening for feed of premixing system 20, underproof organic fertilizer particles is delivered to premixing system 20, the discharge port of drying system 60 is communicated with the opening for feed of cooling system 70, organic fertilizer particles after drying is delivered to cooling system 70, the discharge port of cooling system 70 is communicated with claiming the opening for feed of assembling system 80, claim assembling system 80 organic fertilizer particles is weighed and pack sealing.
Fermentation system in the present embodiment adopts existing fermentation system, as the publication number fixed organic materials fermentation machine that is CN102674921A.Premixing system also adopts existing premixing system, as the publication number material mixer that is CN101462030.If the product that material mixer produces does not meet the charging requirement of a system, can increase again pulverizer mixed material is further pulverized.
As shown in Figure 2, in the present embodiment, a system 30 comprises a machine 31 and fly-ash separator, and a machine 31 comprises housing 32, tripper 33, ball nozzle 34, loading head 35 and hot-air drier 36.Tripper 33, ball nozzle 34, loading head 35 and hot-air drier 36 are all fixedly mounted in housing 32.At the top of housing 32, offer an opening for feed 37, tripper 33 is set under granule opening for feed 37, it is conical that tripper 33 is, and upper end is little, lower end is large, and the tip of tripper 33 is over against granule opening for feed 37.Ball nozzle 34 be positioned at tripper 33 under, ball nozzle 34 connects liquid-storing box by pipeline, on this pipeline, pump is installed, and stores and contain nitrogenous fertilizer or phosphate fertilizer or potash fertilizer or other micro-liquid in liquid-storing box.Liquid in liquid-storing box forms the small liquid particle of atomization by ball nozzle, be sprayed at the pulverulent material falling from the surrounding of tripper 33, forms material granule.Loading head 35 be positioned at ball nozzle 34 under, loading head 35 is funnel-form, the diameter of the opening for feed of loading head 35 upper ends is greater than the diameter of the lower surface of tripper 33, after loading head 35 is collected material granule, perisporium along loading head 35 rolls downwards, form larger bulk particle, these bulk particles are discharged from the discharging of loading head 35 together with powder, and it is flat rectangular-shaped that the discharge port of loading head 35 is.
Hot-air drier 36 is positioned at the below of loading head 35, and the air outlet of hot-air drier 36 is horizontally disposed with, and the air outlet of hot-air drier 36 is over against the discharge port of loading head 35 belows.In the bottom of housing 32, be installed with baffle plate 38, baffle plate 38 is divided into particle chamber 40 and powder chamber 39 by the bottom of housing 32 inner chambers, and baffle plate 38 is positioned at the below of hot-air drier 36.Particle chamber 40 be positioned at loading head 35 discharge port under, powder chamber 39 is positioned at the side-lower of the discharge port of loading head 35, the air outlet of hot-air drier 36 be positioned at particle chamber 40 directly over, and the air outlet of hot-air drier 36 is 39 1 side settings towards powder chamber, by hot-air drier 36 is set, the powder that can play dry bulk particle and other are not formed to bulk particle blows to powder chamber 39 1 sides, thereby realize bulk particle and enter particle chamber 40, pulverulent material enters the object in powder chamber 39.Discharge of fine material mouth 41 is offered in the below in powder chamber 39, and discharge of fine material mouth 41 is connected with fly-ash separator by induced draft fan, and fly-ash separator is collected after powder, again sends into the opening for feed of a machine, carries out granule together with the powder producing with premixing system.Below particle chamber 40, be provided with particulate matter discharge port 42, particulate matter discharge port 42 is communicated with the opening for feed of screening system 50.
In the present embodiment, the discharge port of fermentation system 10 is communicated with the opening for feed of premixing system 20 by the first conveyor, the discharge port of premixing system 20 is communicated with the opening for feed of a system 30 by the second conveyor, the discharge port (namely particulate matter discharge port) of granule system 30 is communicated with the opening for feed of screening system 50 by the 3rd conveyor, the second discharge port of screening system 50 is communicated with the opening for feed of premixing system 20 by the 4th conveyor, the first discharge port of screening system 50 is positioned at the top of the opening for feed of drying system 60, the discharge port of drying system 60 is positioned at the opening for feed top of cooling system 70, the discharge port of cooling system 70 is communicated with claiming the opening for feed of assembling system 80 by the 5th conveyor.
The fermentation mode that the utility model adopts is anaerobically fermenting, adds biological bacteria salt reduction and degreasing simultaneously, and organic substance under anaerobic, forms methane through the fermentative action of microorganism.In the present embodiment, in order to save energy consumption, recycling energy, this production line also comprises burner 90, the air outlet of fermentation system 10 is communicated with the fuel inlet of burner 90, the biogas that fermentation system 10 is produced is delivered to burner 90, and the hot-blast outlet of burner 90 is communicated with the inlet mouth of hot-air drier and the hot air intake of drying system 60 of granule system 30 respectively.
In the present embodiment, cooling system 70 comprises feed screw and blower fan, on the air outlet of blower fan, is fixedly connected with blowpipe, and the other end of air outlet tube gos deep in the opening for feed of feed screw.The rotating cylinder rotation of feed screw, blower fan blowing when particle is pushed ahead, cooling fertilizer.Blower fan can adopt cold blast engine.
Title assembling system in the present embodiment, by screw feeding machine, is transported to organic fertilizer particles in barrel, flows in electronic-weighing cylinder again, and complete pack sealing from barrel.
This production line also comprises Controlling System, and Controlling System and first, second, third, fourth, the 5th conveyor are connected.By Controlling System, control the running of each conveyor, realize the self-feeding of this production line.
Fermentation system in the utility model, premixing system, a system, screening system, drying system, cooling system and title assembling system all can adopt existing mature technology.
Finally it should be noted that: above embodiment only, in order to the technical solution of the utility model to be described, is not intended to limit; Although the utility model is had been described in detail with reference to previous embodiment, those of ordinary skill in the art is to be understood that: its technical scheme that still can record aforementioned each embodiment is modified, or part technical characterictic is wherein equal to replacement; And these modifications or replacement do not make the essence of appropriate technical solution depart from the spirit and scope of each embodiment technical scheme of the utility model.
Claims (7)
1. a full-automatic domestic refuse production organic fertilizer production line, it is characterized in that, comprise fermentation system (10), premixing system (20), granule system (30), screening system (50), drying system (60), cooling system (70) and title assembling system (80), the discharge port of described fermentation system (10) is communicated with the opening for feed of premixing system (20), by fermentation after mass transport to premixing system (20), the discharge port of described premixing system (20) is communicated with an opening for feed for system (30), mixed pulverulent material is delivered to a system, the discharge port of described system (30) is communicated with the opening for feed of screening system (50), the organic fertilizer particles of having rolled into a ball is delivered to screening system (50), the first discharge port of described screening system (50) is communicated with the opening for feed of drying system (60), qualified organic fertilizer particles is delivered to drying system (60), the second discharge port of described screening system (50) is communicated with the opening for feed of premixing system (20), underproof organic fertilizer particles is delivered to premixing system (20), the discharge port of described drying system (60) is communicated with the opening for feed of cooling system (70), organic fertilizer particles after drying is delivered to cooling system (70), the discharge port of described cooling system (70) is communicated with claiming the opening for feed of assembling system (80), described title assembling system (80) is weighed organic fertilizer particles and is packed sealing.
2. full-automatic domestic refuse production organic fertilizer production line according to claim 1, it is characterized in that, described system (30) comprises a machine (31) and fly-ash separator, described machine (31) comprises housing (32), tripper (33), ball nozzle (34), loading head (35) and hot-air drier (36), described tripper (33), ball nozzle (34), loading head (35) and hot-air drier (36) are all fixedly mounted in housing (32), at the top of described housing (32), offer an opening for feed (37), under described opening for feed (37), tripper (33) is set, it is conical that described tripper (33) is, the tip of tripper (33) is over against granule opening for feed (37), described ball nozzle (34) be positioned at tripper (33) under, described loading head (35) be positioned at ball nozzle (34) under, described loading head (35) is funnel-form, the diameter of the opening for feed of described loading head (35) upper end is greater than the diameter of the lower surface of tripper (33), described hot-air drier (36) is positioned at the below of loading head (35), the air outlet of hot-air drier (36) is horizontally disposed with, the air outlet of hot-air drier (36) is over against the discharge port of loading head (35) below, in the bottom of described housing (32), be installed with baffle plate (38), described baffle plate (38) is divided into particle chamber (40) and powder chamber (39) by the bottom of housing (32) inner chamber, described baffle plate (38) is positioned at the below of hot-air drier (36), described particle chamber (40) be positioned at loading head (35) discharge port under, described powder chamber (39) is positioned at the side-lower of the discharge port of loading head (35), the air outlet of described hot-air drier (36) be positioned at particle chamber (40) directly over, and the air outlet of hot-air drier (36) is (39) one side settings towards powder chamber, discharge of fine material mouth (41) is offered in the below in described powder chamber (39), described discharge of fine material mouth (41) is connected with fly-ash separator by induced draft fan, the below in described particle chamber (40) is provided with particulate matter discharge port (42), described particulate matter discharge port (42) is communicated with the opening for feed of screening system (50).
3. full-automatic domestic refuse production organic fertilizer production line according to claim 1 and 2, it is characterized in that, the discharge port of described fermentation system (10) is communicated with the opening for feed of premixing system (20) by the first conveyor, the discharge port of described premixing system (20) is communicated with an opening for feed for system (30) by the second conveyor, the discharge port of described system (30) is communicated with the opening for feed of screening system (50) by the 3rd conveyor, the second discharge port of described screening system (50) is communicated with the opening for feed of premixing system (20) by the 4th conveyor, the discharge port of described cooling system (70) is communicated with claiming the opening for feed of assembling system (80) by the 5th conveyor.
4. full-automatic domestic refuse production organic fertilizer production line according to claim 3, it is characterized in that, also comprise burner (90), the air outlet of described fermentation system (10) is communicated with the fuel inlet of burner (90), the biogas that fermentation system (10) is produced is delivered to burner (90), and the hot-blast outlet of described burner (90) is communicated with the inlet mouth of hot-air drier and the hot air intake of drying system (60) of granule system (30) respectively.
5. full-automatic domestic refuse production organic fertilizer production line according to claim 4, it is characterized in that, described cooling system (70) comprises feed screw and blower fan, on the air outlet of described blower fan, be fixedly connected with blowpipe, the other end of described air outlet tube gos deep in the opening for feed of feed screw.
6. full-automatic domestic refuse production organic fertilizer production line according to claim 5, is characterized in that, described blower fan is cold blast engine.
7. full-automatic domestic refuse production organic fertilizer production line according to claim 6, is characterized in that, also comprise Controlling System, described Controlling System and first, second, third, fourth, the 5th conveyor are connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420440925.3U CN203976655U (en) | 2014-08-06 | 2014-08-06 | Full-automatic domestic refuse production organic fertilizer production line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420440925.3U CN203976655U (en) | 2014-08-06 | 2014-08-06 | Full-automatic domestic refuse production organic fertilizer production line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203976655U true CN203976655U (en) | 2014-12-03 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420440925.3U Expired - Fee Related CN203976655U (en) | 2014-08-06 | 2014-08-06 | Full-automatic domestic refuse production organic fertilizer production line |
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| CN (1) | CN203976655U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113732018A (en) * | 2021-09-03 | 2021-12-03 | 北京嘉博文生物科技有限公司 | Continuous organic garbage biological treatment machine |
-
2014
- 2014-08-06 CN CN201420440925.3U patent/CN203976655U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113732018A (en) * | 2021-09-03 | 2021-12-03 | 北京嘉博文生物科技有限公司 | Continuous organic garbage biological treatment machine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141203 Termination date: 20200806 |